AU730283B2

AU730283B2 - Process for the preparation of a foodstuff by extrusion

Info

Publication number: AU730283B2
Application number: AU28352/97A
Authority: AU
Inventors: Osvaldo Geromini; Ernst Heck; Werner Pfaller
Original assignee: Societe des Produits Nestle SA; Nestle SA
Current assignee: Societe des Produits Nestle SA
Priority date: 1996-06-30
Filing date: 1997-06-27
Publication date: 2001-03-01
Anticipated expiration: 2017-06-27
Also published as: KR100424928B1; PT815747E; HU9701126D0; HU222612B1; ZA975697B; HUP9701126A3; CA2209346A1; AR007682A1; RU2178981C2; SI0815747T1; EP0815747A1; DE69611034D1; ES2153075T3; NO973015L; ATE197663T1; JPH1057038A; NO973015D0; CA2209346C; CZ207197A3; PL183659B1

Description

1

AUSTRALIA

PATENTS ACT 1990 COMPLETE SPECIFICATION FOR A STANDARD PATENT

ORIGINAL

'4 *r S 4 4 4 Name of Applicant/s: Actual Inventor/s: Address of Service: Invention Title: Societe Des Produits Nestle S.A.

Ernst HECK, Osvaldo GEROMINI and Werner PFALLER SHELSTON WATERS MARGARET STREET SYDNEY NSW 2000 "PROCESS FOR THE PREPARATION OF A FOODSTUFF BY

EXTRUSION"

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4** The following statement is a full description of this invention, including the best method of performing it known to us:- (File: 19681.00) -la- PROCESS FOR THE PREPARATION OF A FOODSTUFF BY EXTRUSION The subject of the present invention is a process for the preparation of a foodstuff by extrusion and an installation for carrying out the process.

EP0262300 describes a process and an installation for producing a mass of chocolate, which involve the use of an extruder split into zones in which the successive steps of sterilising and deodorising pieces of raw beans using pressurised steam, roasting the pieces of beans having reduced them to a powder in a hammer mill connected in parallel with two zones which are separated by an element of screw with a flight of opposite hand, adding and mixing powdered sugar to the roasted bean powder, adding cocoa butter, mixing and extrusion are carried out.

It is an object of the present invention to overcome or ameliorate at least one of •.o *o the disadvantages of the prior art, or to provide a useful alternative.

S: Accordingly, there is provided a process for the preparation of a foodstuff by extrusion, in which a food substance is introduced into, mixed and cooked in a first '00 15 section of a twin-screw extruder, the cooking of the mass obtained is prolonged in a 0 o cooker connected up in series with the first section and a second section of the extruder 0 0 dynamically separated from the first, the cooked mass is then introduced into the second section, the mass is extruded by passing it through a die and then the extruded product is o cut.

Likewise, the installation according to the present invention comprises a twinscrew extruded split into two distinct sections by a dynamic-separation device, a cooker connected in parallel with the first section and the second section, a die and a cutting device.

Such a process and such a piece of equipment effectively allow efficient use of a twin-sciew 2 extruder which use is particularly well suited to the preparation of cooked-extruded foodstuffs with a good cooked flavour.

In this description, the expression "food substance" covers all the components introduced together or separately, at the same time or in succession, into the first section of the extruder and processed all together at least in a part of this section.

In order to carry out the current process, it is possible to start with food substances from which it is possible to produce, by extrusion, the widest possible range of foodstuffs such as breakfast cereals, children's cereals, snacks, crumb coatings, confectionery or products for domestic animals, for example.

The components and their respective proportions can be chosen, and these substances can then be "processed in the extruder under conditions of pressure, shear and temperature which are chosen to suit the 20 characteristics of the product to be obtained, especially as a function of the water content and degree S"of expansion which is to be obtained after the die.

It is also possible to keep back ingredients which are sensitive to heat such as vitamins or colourings which form part of the composition of the product and not introduce them into the cooked mass until the second section, for example.

It is possible to process in the first section of the extruder a substance which has a water content of 18 25%, to maintain this water content in the cooker and to reduce it to 14 22% in the second section by the release of steam in order to obtain an expanded product, for example.

Such a cut expanded product may be dehydrated down to a water content of less than for example.

It is possible to process in the first section of the extruder a substance which has a water content of 24 36%, and to maintain this water content in the 3 cooker and in the second section in order to obtain a little- or non-expanded product, for example.

Such a cut little- or non-expanded product may be converted into flakes by rolling and toasting, for example.

The installation for carrying out the process according to the present invention therefore comprises a twin-screw extruder split into two distinct sections by a dynamic-separation device, a cooker connected in parallel with the first section and the second section, an extrusion die and a cutting device.

The dynamic-separation device may be produced in the form of a blocking zone where the twin-screw unit is of opposite hand, for example.

In this embodiment of the dynamic-separation device, provision may be made for an outlet from the first section of the extruder to straddle a compression .i zone and the blocking zone of the twin-screw unit, for example.

20 Provision may be made for an outlet from the second section to be along the axis of or to the side of S"the downstream end of the extruder, for example.

The outlet from the second section may lead directly to the die or be connected thereto by an appropriate duct, for example.

Provision may be made for there to be a feed device for the first section, in the form of one or more feed openings provided in a barrel of the twin-screw unit, starting from the upstream end of the extruder. An 30 opening for returning or inletting the cooked mass into the second section may be provided in the barrel of the twin-screw unit, near a transport zone following the blocking zone of the twin-screw unit, for example.

It is possible to provide, near the inlet of the second section, a device for exhausting or releasing steam in the form of a vacuum suction pipe connected to a pump, an opening directly to the atmosphere or a backpressure valve, for example.

4 The cooker may be connected up in parallel with the first section and the second section via appropriate ducts linking one inlet of the cooker to the outlet of the first section and one outlet of the cooker to the inlet of the second section.

It is possible to envisage a screw geometry which, for each section, is adapted to suit the substance to be processed and the product which is to be obtained. In particular, successive and/or alternating zones for transporting, compacting, compressing, kneading or mixing, for example, may be envisaged. To define these various zones, the pitch of the screws, the space left empty for the substance to be processed, defined especially by the respective diameters of the shafts and of the flights, may be altered, or bilobes of varying shapes may be inserted, for example. It is also possible to alter a subdivision of the barrel of the extruder in several independent compartments, the :-.-.temperature of which may be adjusted individually by 20 circulating a cooling or heating fluid, for example.

Finally, the mechanical energy needed to process the food substance in the first section of the twinscrew unit, to process the cooked mass in the second section and to pass the mass through the die may be supplied by a single means of driving the screws of the twin-screw unit, such as an electric motor for example.

To pass the mass of cooked food substance through a die, this motor may be assisted or the load on it may be lightened using a positive-displacement pump 30 such as a gear pump connected upstream of the die, for example.

The installation according to the present invention is described hereinbelow with reference to the appended drawing in which: Figure 1 diagrammatically represents one embodiment of the installation intended for the preparation of an expanded product, 5 Figure 3 diagrammatically represents one embodiment of the geometry of the screws of the installation according to Figure 1, Figure 4 diagrammatically represents one embodiment of the geometry of the screws of the installation according to Figure 2, Figure 5 represents in greater detail the embodiment of the dynamic-separation device of the screws represented in Figures 3 and 4.

In the embodiment represented in Figure 1, the present installation comprises a twin-screw extruder split into two distinct sections 1 and 2 by a dynamicseparation device 3, a cooker 4 connected in parallel with the first section 1 and with the second section 2, a die 5 and a cutting device, not represented.

The cooker may be produced in the form of a double-walled holding tube or of a double-walled .i •ehorizontal cylindrical bath containing an Archimedean screw driven by a motor, for example.

The twin-screw unit is driven by a motor 6 and is contained in a double-walled barrel subdivided into seven compartments i-vii, in each of which a cooling or heating fluid can be circulated.

In this installation, a substance A is introduced into the first section 1 of the extruder through a feed device comprising a feed opening 7 provided in the first compartment i of the barrel. The mass of substance A processed in the first section 1 leaves the extruder through an outlet 8 provided in the 30 compartment iv of the barrel at the location of the dynamic-separation device 3 and connected to an inlet 41 into the cooker 4.

The mass cooked in the cooker leaves this cooker via an outlet 42 connected to an opening 9 for returning or inleting the cooked mass into the second section 2 of the extruder, this opening being provided in the fifth compartment v of the barrel, downstream of the dynamicseparation device 3.

6 At the inlet to the second section 2, the water content of the mass of cooked substance is reduced by means of a device for exhausting or releasing steam comprising a vacuum suction pipe 31 connected to a pump, not represented.

The mass of substance processed in the second section 2 leaves the extruder via an outlet 10 provided along the axis of its downstream end and connected to the die 5 on exit from which it can expand.

In the embodiment represented in Figure 2, the present installation does not have a device for exhausting or releasing steam. In addition, by comparison with the embodiment represented in Figure 1, it has differences as regards the geometry of the screws.

In this. installation which is intended for the preparation of a little- or non-expanded product, the ""cooked mass from the cooker therefore has no steam exhausted and/or is not partially dehydrated as it o* 20 enters the second section of the extruder.

In the embodiment represented in Figure 3, the S"geometry of the screws is similar over a large part of the two sections 1 and 2 of the extruder, but has :°ooo o significant differences near the respective outlets from these sections.

In section 1, the screws have, in succession, a transport zone 11 (200/100), a compacting zone 12 (100/50), a compression zone 13 (100/33), an intermediate transport zone 14 (100/66), a compression zone 15 (100/35 200/28), a kneading zone 16 (100/-33), a compression zone 17 (100/35), an expulsion zone 18 (three-off 12.5 bilobes), and a blocking zone 3 (100/- In section 2, the screws have, in succession, a compacting zone 12 (50/50), a transport zone 11 (200/100), a compression zone 13 (100/33), a transport zone 14 (100/66), and a compression zone 15 (100/35 200/28 100/33 100/35) 7 The figures given in brackets give the length of the zone and the pitch in mm, for screws 88 mm in diameter and a distance of 72 mm between axes, the installation in this case comprising a CLEXTRAL BC-72 S twin-screw extruder.

The geometry represented is not limited to these dimensions which are given by way of example. It may be transposed onto other models of extruder, especially the models BC-45 (screws 55 mm in diameter, with a distance of 45 mm between axes) or BC-72 (screws 115 mm in diameter, with a distance of 92 mm between axes) of the same series, for example.

The screw flights are preferably double, except for the opposite-handed flight in the blocking zone which is preferably single.

In contrast to the opposite-handed flight in the kneading zone 16 which on its periphery has cutouts for .the passage of the processed mass, the opposite-handed :flight in the blocking zone 3 has none in order that it 20 can be as efficient as possible in fulfilling its role as a dynamic-separation device.

.The outlet 8 from the first section 1 of the extruder has an axial oblong shape, in this case the shape of a figure eight, covering the entire length of 25 the expulsion zone 18, straddling the compression zone 17 and the blocking zone 3.

The inlet opening 9 into the second section 2 also has an axial oblong shape, in this case also the shape of a figure eight.

30 In the embodiment represented in Figure 4, the geometry of the screws in the second section 2 of the extruder is similar to that represented in Figure 3. By contrast, the geometry of the screws in the first section 1 differs from this as regards the compression zone 15 (100/35 50/35 100/28 instead of 100/35 200/28). It also differs from the geometry of Figure 3 as regards the zone 16 which here is a mixing zone formed of 10 bilobes 15 mm thick, instead of a kneading zone.

8 Figure 5 shows in greater detail how the outlet 8 from the first section 1 of the extruder covers the entire length of the expulsion zone 18, straddling the compression zone 17 and the blocking zone 3. In particular it has been observed that it is essential for this opening to overlap the blocking zone 3, by a fraction of the length of the opening which corresponds approximately to 0.1 0.3 times the diameter of the screw, for example, so that the substance taken up by the first flight or flights of the opposite-handed screw can be discharged and expelled effectively.

It is also important, to ensure good dynamic separation, for the blocking zone to be long enough, namely for it to have a length at least equal to the diameter of the screws, for an opposite-handed screw flight of between approximately 1/5 and 1/3 of this diameter, for example.

The examples below are given by way of an illustration of the process according to the present invention and of the products which can be obtained thereby. The percentages and parts therein are given by weight.

In these examples, the oil may be chosen, if need be, as a function of the physical purpose it has in the processed and extruded mass, and as a function of its taste, neutral or otherwise. It may be chosen from palm kernel oil, groundnut oil or corn oil, for example.

In these examples too, the mixture of flours, the oil and the water are introduced, as appropriate, 30 individually into the feed opening of the extruder.

Example 1 Use is made of an installation like the' one represented in Figures 1 and 3. The extrusion die is made in the form of a pierced plate having 4 cylindrical extrusion ducts 3.0 mm in diameter.

This installation is used to prepare breakfast cereals with the ingredients and under the conditions given in Tables la) and Ib) below.

9- Table la) gives the ingredients of a mixture of flours, their proportions in a typical mixture and the possible ranges of their proportions.

Table Ib) gives the quantities of the ingredients introduced into the extruder, the water content of the substance or of the processed mass and the operating conditions in each section.

Table la): Mixture of flours

LO

Ingredients Typical mixture Possible range Cornflour 20 0-80 Wheat flour 64 0-80 Oatmeal 10 0-80 Sugar 4.9 2-12 Salt 1 1-3 Vitamins and 0.1 0.1-0.2 trace elements Total 100 100 0 0 0 I. 0* 10 Table lb): Operating conditions

S

C.

S.

S..

C

C. i. Parameter Units Value Possible range Mixture of flours kg/h 230 200-350 Palm kernel oil kg/h 18 15-30 Water kg/h 42 40-65 Water content of mass 1" section 23.2 18-25 Rotational speed of screws rpm 360 250-450 Temperature of mass 1 section 0 C 145 140-170 Pressure of mass I st section bar 85 60-100 Temperature of mass 2" section 0 C 158 150-180 Pressure of mass 2 nd section bar 112 80-130 Current A 291 250-450 Vacuum inlet 2 nd section mbar 450 150-1000 Reduced water content mass 2" section 18.5 14-22 Residence time cooker min 35 20-45 Temperature cooker 0 C 130 120-150 Density extruded product g/l 108 60-140 Breakfast cereals in the shape of small balls 8 to 12 mm in diameter with a good cooked taste are thus obtained.

Example 2 Use is made of an installation like the one represented in Figures 2 and 4. The extrusion die is made in the form of a plate pierced with 12 cylindrical extrusion ducts 4.0 mm in diameter.

This installation is used to prepare breakfast cereals with the ingredients and under the conditions given in Tables 2a) and 2b) below.

Table 2a) gives the ingredients of a mixture of flours, their proportions in a typical mixture, and the possible ranges of their proportions.

Table 2b) gives the quantities of ingredients introduced into the extruder, the water content of the substance or of the processed mass and the operating I 1, 11 conditions in each section. Steam is injected into the first section in the region of the intermediate transport zone 14. There is no vacuum suction at the inlet to the second section.

Table 2a): Mixture of flours Typical Possible Ingredients mixture range Cornflour 91 85-98 Sugar 6.9 0-12 Salt 2 0-3 Vitamins and 0.1 0.1-0.2 trace elements Total 100 100 Table 2b): Operating conditions -b Parameter Units Value Possible range Mixture of flours kg/h 240 200-350 Steam kg/h 15 0-35 Water kg/h 32 25-60 Water content of mass 25.6 24-36 Rotational speed of screws rpm 195 140-250 Temperature of mass 1 t section 0 C 125 115-140 Pressure of mass 1 I section bar 50 40-70 Temperature of mass 2 d section OC 91 80-100 Pressure of mass 2 d section bar 71 50-80 Current A 156 120-250 Residence time cooker min 35 20-50 Temperature cooker 0 C 100 80-100 Density extruded product g/l 685 600-750 Little- or non-expanded cereal balls with a diameter of approximately 5mm that can be converted 12 into flakes with a good cooked flavour by rolling and toasting are thus obtained.

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Claims

1. Process for the preparation of a foodstuff by extrusion, in which a food substance is introduced into, mixed and cooked in a first section of a twin-screw extruder, the cooking of the mass obtained is prolonged in a cooker connected up in series with the first section and a second section of the extruder dynamically separated from the first, the cooked mass is then introduced into the second section, the mass is extruded by passing it through a die and then the extruded product is cut.

2. Process according to Claim 1, in which a substance which has a water content of

18-25% is processed in the first section of the extruder, this water content is maintained in the cooker and reduced to 14-22% in the second section by the release of steam in order to obtain an expanded product. down to a water content of less than 4. Process according to Claim 1, in which a substance which has a water content of 15 24-36% is processed in the first section of the extruder, and this water content is maintained in the cooker and in the second section in order to obtain a little or non- expanded product. Process according to Claim 4, in which the cut little or non-expanded product is converted into flakes by rolling and toasting. 20 6. Installation for carrying out the process according to Claim 1, comprising an e e :extruder split into two distinct sections by a dynamic-separation device, wherein the first and second sections both rely on a common pair of screws, a cooker connected in series with the first section and the second section, a die and a cutting device. 7. Installation according to Claim 6, in which the dynamic-separation device comprises a blocking zone where the twin-screw unit is of opposite hand. 14 8. Installation according to Claim 7, in which an outlet from the first section of the extruder straddles a compression zone and the blocking zone of the twin- screw unit. 9. A process for the preparation of a foodstuff substantially as herein described with reference to any one of the examples. An installation for the preparation of a foodstuff substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings. DATED this 27th Day of June, 1997 SOCIETE DES PRODUITS NESTLE S.A. Attorney? IAN ERNST Fellow Institute of Patent Attorneys of Australian of SHELSTON WATERS o•